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CO2‐resistant SDC‐SSAF oxygen selective dual‐phase hollow fiber membranes
Asia-Pacific Journal of Chemical Engineering ( IF 1.8 ) Pub Date : 2020-06-11 , DOI: 10.1002/apj.2528
Shude Zhang 1 , Claudia Li 2, 3 , Xiuxia Meng 1 , Xiaoyao Tan 4 , Zhonghua Zhu 5 , Jaka Sunarso 2 , Shaomin Liu 3, 6
Affiliation  

Ce0.85Sm0.15O1.925–Sm0.6Sr0.4Al0.3Fe0.7O3‐δ (SDC‐SSAF) hollow fiber membranes aimed for oxyfuel application are fabricated via a phase inversion‐sintering technique using powders synthesized from EDTA–citrate complex method. Oxygen ions transport is revealed to be the limiting step that determines the overall oxygen transport rate in SDC‐SSAF. SDC‐SSAF hollow fiber membrane attained a maximum flux of 2.6 ml min−1 cm−2 at 950°C under an oxygen partial pressure difference of 1/0.02 atm (feed/permeate). Variation in oxygen partial pressure on the permeate side exerts larger influence on the oxygen permeation flux relative to the change on the feed side. Stability tests over 100 h demonstrate stable oxygen permeation flux under both He and CO2 sweep conditions.

中文翻译:

耐CO2的SDC-SSAF氧气选择性双相中空纤维膜

的Ce 0.850.15 ö 1.925 -Sm 0.60.4的Al 0.3的Fe 0.7 ø 3-δ旨在用于富氧燃烧应用(SDC-SSAF)中空纤维膜是通过使用从EDTA-柠檬酸络方法合成的粉末倒相烧结技术制造。氧离子传输被认为是决定SDC-SSAF中总氧传输速率的限制步骤。SDC-SSAF中空纤维膜的最大通量为2.6 ml min -1 cm -2在950°C的条件下,氧气分压差为1 / 0.02 atm(进料/渗透液)。相对于进料侧的变化,渗透侧的氧气分压的变化对氧气的渗透通量产生更大的影响。超过100小时的稳定性测试表明,在He和CO 2吹扫条件下,氧气的渗透通量都稳定。
更新日期:2020-06-11
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